CA1336645C - Process and apparatus for the preparation of synthesis gas - Google Patents
Process and apparatus for the preparation of synthesis gasInfo
- Publication number
- CA1336645C CA1336645C CA000564586A CA564586A CA1336645C CA 1336645 C CA1336645 C CA 1336645C CA 000564586 A CA000564586 A CA 000564586A CA 564586 A CA564586 A CA 564586A CA 1336645 C CA1336645 C CA 1336645C
- Authority
- CA
- Canada
- Prior art keywords
- lockhopper
- slag
- gas
- quench vessel
- valves
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/46—Gasification of granular or pulverulent flues in suspension
- C10J3/48—Apparatus; Plants
- C10J3/52—Ash-removing devices
- C10J3/526—Ash-removing devices for entrained flow gasifiers
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/46—Gasification of granular or pulverulent flues in suspension
- C10J3/48—Apparatus; Plants
- C10J3/485—Entrained flow gasifiers
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/72—Other features
- C10J3/82—Gas withdrawal means
- C10J3/84—Gas withdrawal means with means for removing dust or tar from the gas
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/08—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors
- C10K1/10—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids
- C10K1/101—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids with water only
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2200/00—Details of gasification apparatus
- C10J2200/15—Details of feeding means
- C10J2200/156—Sluices, e.g. mechanical sluices for preventing escape of gas through the feed inlet
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
- C10J2300/0913—Carbonaceous raw material
- C10J2300/093—Coal
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
- C10J2300/0953—Gasifying agents
- C10J2300/0956—Air or oxygen enriched air
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
- C10J2300/0953—Gasifying agents
- C10J2300/0959—Oxygen
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Processing Of Solid Wastes (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
- Gasification And Melting Of Waste (AREA)
Abstract
A process for the preparation of synthesis gas by partial combustion of finely divided solid carbon-containing fuel with an oxygen-containing gas in a reactor. The liquid slag formed during the partial combustion process falls into a water bath or slag quench vessel where it solidifies and from there falls by gravity into a lockhopper from which the solidified slag is batchwise sluiced out of the gasification system. A gas bubble or gascap is created and maintained in the lockhopper, the pressure of the gas bubble being lower than the pressure in the slag quench vessel.
Thus an initial downwards flow of water and slag is created during opening of the valves between the lockhopper and the slag quench vessel.
Thus an initial downwards flow of water and slag is created during opening of the valves between the lockhopper and the slag quench vessel.
Description
--- 1 1 3 3 6 6 4 s PROCESS AND APPARATUS FOR THE PREPAR~TION
OF SYNTHESIS GAS
m e invention relates to a process for the preparation of synthesis gas by the partial combustion of a finely divided solid carbon-containing fuel with an oxygen-containing gas in a reactor wherein liquid slag formed during the partial combustion process is removed through an outlet in the bottom of the reactor and passed by gravity through a slag ~ h~rge means into a water bath or slag quenching vessel where it is sol;~;f;e~ by quenching.
m e partial combustion of finely divided solid carbon-contain-ing fuel with substantially pure oxygen as oxygen-containing gas yields synthesis gas mainly consisting of carbon monoxide and h~dluy~l. When the oxygen-containing gas is air or oxygen-enriched air, the synthesis gas formed of course also contains a substantial quantity of nitrogen. By finely divided solid carbon-containing fuel is generally meant coal or another solid fuel, such as brown coal, peat, wood, coke, soot etc., but mixtures of liquid or gas and particulate solid fuels, are also possible.
Advantageously, a mcderator is also introduced into the reactor. m e object of the mcderator is to exercise a moderating effect on the temperature on the reactor. miS is ensured by endothermic reaction between the mcderator and the reactants and/or products of the synthesis gas preparation. Suitable moderators are steam and carbon ~;nx;~.
The gasification is advantageously carried out at a tempera-ture in the range from 1200 to 1700 C and at a pressure in the range from 1 to 200 bar.
The reactor in which the preparation of synthesis gas takes place may have any suitable shape.
- _ 1 336645 m e supply of finely divided solid carbon-containing fuel and oxygen-containing gas to the reactor can take place in any manner suitable for the purpose and will not be described in detail.
Liquid slag fonmed in the partial combustion reaction drops down and is drained through the outlet located in the reactor bottom.
To remove the slag from the gasifying process, it is already known to arrange a quenching water bath or slag quench vessel located below the reactor and connected therewith in any way suitable for the purpo æ , in which water bath or slag quench ves æ l the slag descending due to its gravity, is captured, quenched, and forms clinker granules or agglcmerations. After such granulation, the clinker is periodically or continuously removed fram the said water bath or slag quench vessel by means of o~lv~-Lional arrangements.
m is may for example be carried out by means of a lockhopper from which solidified slag is batchwise sluiced out of the gasification system.
During the sluicing cycle the lockhopper is isolated from the gasification system by closing one or more valves in the connecting line between the slag quench vessel and the lockhopper.
However, the slag which is produced in the meantime in the partial combustion process collects in the slag quench ves æ l above these valves where it shows a tendency for bridging at the narrow space just above the said valves.
However, it has appeared very difficult to have the slag to fall into the lockhopper after reconnecting the lockhopper to the gasification system.
Even water jet nozzles for agitation purpo æs proved to be not successful. Therefore, it is an object of the invention to provide a process and an apparatus for pro~ ing synthesis gas by the partial ccmbustion of finely divided solid carbon-containing fuel wherein the liquid slag formed during the partial combustion process can be removed from the slag quench ves æ l easily in a very effective and efficient manner.
3 63293-2g39 It is another object of the invention to provide a quick performance test of the valves between the slag quench vessel and the lockhopper.
The invention therefore provides a process for the preparation of synthesis gas by partial combustion of finely divided solid carbon-containing fuel with an oxygen-containing gas in a reactor, wherein liquid slag formed during the partial combustion process falls into a water bath or slag quench vessel where it solidifies and from there falls by gravity into a lockhopper from which the solidified slag is batchwise sluiced out of the gasification system, said lock-hopper and slag quench vessel being connected through one or more valves, comprising the steps of creating and maintaining a gas bubble or gascap in the lockhopper, the pressure of the gas bubble being lower than the pressure in the slag quench vessel when the said one or more valves between the lockhopper and the slag quench vessel are closed, thus creating an initial downwards flow of water and slag during opening of the valves between the lockhopper and the slag quench vessel.
The invention also provides an apparatus for carrying out the above process comprising a slag quench vessel, connected through one or more valves to a lockhopper provided at its bottom with an outlet comprising one or more valves, and means for creating and maintaining a gas bubble or gascap in the lockhopper.
In an advantageous embodiment of the invention the gas bubble in the lockhopper can be created by inserting downwardly a pipe of a certain length into the top of the lockhopper.
In another advantageous embodiment the gas bubble 3a 1 3 3 6 6 4 5 63293-2939 consists of an inert gas such as nitrogen.
The invention will now be described in more detail, by way of example only, with reference to the accompanying drawings, in which:
Figures 1 and 2 schematically represent advantageous embodiments of the apparatus of the invention.
Referring now to Figures 1 and 2 a cross-section of a slag quench vessel 1 provided with an outlet 2 has been represented. The slag quench vessel 1 is part of a gasification system and is located below a reactor or gasification zone wherein the partial combustion process is carried out, and is connected thereto in any manner suitable for the purpose.
me g~s;fiG~tion zone has not been represented for reasons of clarity. me outlet 2 of the slag quench vessel l is connected by any suitable connecting line 3 to a lockhopper 4 located below the said slag quench vessel. In the line 3 one or more valves 3a are provided.
In the lockhopper 4 a pprm~npnt gas bubble or gascap 5 is maintained, at a pressure lower than the pressure in the slag quench vessel l. The gas bubble may for example consist of an inert gas such as nitrogen.
The lockhopper 4 is provided with an outlet 7 at its bottom and one or mnre valves 7a for discharging the solidified slag from the gasification system during a sluicing cycle. m e slag can be discharged to any means suitable for the purpose (not shown for reasons of clarity). The gas bubble 5 in the lockhopper may be maintained by supplying inert gas (such as nitrogen) to the lockho~per 4 by means of a conduit or pipe 6 penetrating into the upper interior space of the lockhopper, as shown in fig. l, or advantageously by means of a pipe 6a in fluid communication with the vertically disposed conduit between the slag quench vessel l and the lockhopper 4, as shown in fig. 2, and wherein said vertical conduit penetrates into the interior of said lockh~ppPr a distance sufficient to maintain the gas bubble in the ll~pprmnst part of the lockhopper.
m e operation of the system of the invention is as follows:
the liquid slag which is formed in the gasification system during the partial combustion process falls into the water bath or slag quench vessel l where it soli~ifies.
From the slag quench vessel l it falls by gravity into the lockhopper 4 from which the solidified slag is batchwise sluiced out of the gasification system. It will be clear to those skilled in the art that at ~Lu~Liate times the valves 3a and 7a should be opened and closed respectively.
~uring the sluicing cycle the lockhopper 4 is isolated from -the g~ific~tion system since the valves 3a between the slag quench vessel and the lockhopper are closed, whereas the valves 7a at the outlet 7 of the lockhopper 4 are opened. m us, slag which is produced in the meantime, will collect in the slag quench vessel 1 above the valves 3a and has a tendency for bridging at the narrow space just abcve these valves ( schematically represented by the bridging region A).
According to the invention, after reconnecting the lockhopper 4 to the gasification system by closing the valves 7a and opening the valves 3a the gas bubble in the lockhopper having a lower pressure than the pressure in the slag quench vessel creates an initial downwards flow of water and slag thus resulting in a debridging action in the region A.
It will be appreciated that the gas bubble also allows a quick performance test of the valves. If the volume of the gas bubble changes with time this is an indication of valve leakages.
It will further be appreciated that the pressure of the gas bubble in the lockhopper can be higher than the pressure of the discharge means outside the lockhopper. In this manner unloading of the lockhopper is facilitated and possible bridging at the outlet 7 of the lockhopper is reduced.
Various mn~if;c~tions of the present invention will hec~mP
apparent to those skilled in the art from the foregoing description and accompanying drawing. Such modifications are intended to fall within the scope of the ~pe~d claims.
OF SYNTHESIS GAS
m e invention relates to a process for the preparation of synthesis gas by the partial combustion of a finely divided solid carbon-containing fuel with an oxygen-containing gas in a reactor wherein liquid slag formed during the partial combustion process is removed through an outlet in the bottom of the reactor and passed by gravity through a slag ~ h~rge means into a water bath or slag quenching vessel where it is sol;~;f;e~ by quenching.
m e partial combustion of finely divided solid carbon-contain-ing fuel with substantially pure oxygen as oxygen-containing gas yields synthesis gas mainly consisting of carbon monoxide and h~dluy~l. When the oxygen-containing gas is air or oxygen-enriched air, the synthesis gas formed of course also contains a substantial quantity of nitrogen. By finely divided solid carbon-containing fuel is generally meant coal or another solid fuel, such as brown coal, peat, wood, coke, soot etc., but mixtures of liquid or gas and particulate solid fuels, are also possible.
Advantageously, a mcderator is also introduced into the reactor. m e object of the mcderator is to exercise a moderating effect on the temperature on the reactor. miS is ensured by endothermic reaction between the mcderator and the reactants and/or products of the synthesis gas preparation. Suitable moderators are steam and carbon ~;nx;~.
The gasification is advantageously carried out at a tempera-ture in the range from 1200 to 1700 C and at a pressure in the range from 1 to 200 bar.
The reactor in which the preparation of synthesis gas takes place may have any suitable shape.
- _ 1 336645 m e supply of finely divided solid carbon-containing fuel and oxygen-containing gas to the reactor can take place in any manner suitable for the purpose and will not be described in detail.
Liquid slag fonmed in the partial combustion reaction drops down and is drained through the outlet located in the reactor bottom.
To remove the slag from the gasifying process, it is already known to arrange a quenching water bath or slag quench vessel located below the reactor and connected therewith in any way suitable for the purpo æ , in which water bath or slag quench ves æ l the slag descending due to its gravity, is captured, quenched, and forms clinker granules or agglcmerations. After such granulation, the clinker is periodically or continuously removed fram the said water bath or slag quench vessel by means of o~lv~-Lional arrangements.
m is may for example be carried out by means of a lockhopper from which solidified slag is batchwise sluiced out of the gasification system.
During the sluicing cycle the lockhopper is isolated from the gasification system by closing one or more valves in the connecting line between the slag quench vessel and the lockhopper.
However, the slag which is produced in the meantime in the partial combustion process collects in the slag quench ves æ l above these valves where it shows a tendency for bridging at the narrow space just above the said valves.
However, it has appeared very difficult to have the slag to fall into the lockhopper after reconnecting the lockhopper to the gasification system.
Even water jet nozzles for agitation purpo æs proved to be not successful. Therefore, it is an object of the invention to provide a process and an apparatus for pro~ ing synthesis gas by the partial ccmbustion of finely divided solid carbon-containing fuel wherein the liquid slag formed during the partial combustion process can be removed from the slag quench ves æ l easily in a very effective and efficient manner.
3 63293-2g39 It is another object of the invention to provide a quick performance test of the valves between the slag quench vessel and the lockhopper.
The invention therefore provides a process for the preparation of synthesis gas by partial combustion of finely divided solid carbon-containing fuel with an oxygen-containing gas in a reactor, wherein liquid slag formed during the partial combustion process falls into a water bath or slag quench vessel where it solidifies and from there falls by gravity into a lockhopper from which the solidified slag is batchwise sluiced out of the gasification system, said lock-hopper and slag quench vessel being connected through one or more valves, comprising the steps of creating and maintaining a gas bubble or gascap in the lockhopper, the pressure of the gas bubble being lower than the pressure in the slag quench vessel when the said one or more valves between the lockhopper and the slag quench vessel are closed, thus creating an initial downwards flow of water and slag during opening of the valves between the lockhopper and the slag quench vessel.
The invention also provides an apparatus for carrying out the above process comprising a slag quench vessel, connected through one or more valves to a lockhopper provided at its bottom with an outlet comprising one or more valves, and means for creating and maintaining a gas bubble or gascap in the lockhopper.
In an advantageous embodiment of the invention the gas bubble in the lockhopper can be created by inserting downwardly a pipe of a certain length into the top of the lockhopper.
In another advantageous embodiment the gas bubble 3a 1 3 3 6 6 4 5 63293-2939 consists of an inert gas such as nitrogen.
The invention will now be described in more detail, by way of example only, with reference to the accompanying drawings, in which:
Figures 1 and 2 schematically represent advantageous embodiments of the apparatus of the invention.
Referring now to Figures 1 and 2 a cross-section of a slag quench vessel 1 provided with an outlet 2 has been represented. The slag quench vessel 1 is part of a gasification system and is located below a reactor or gasification zone wherein the partial combustion process is carried out, and is connected thereto in any manner suitable for the purpose.
me g~s;fiG~tion zone has not been represented for reasons of clarity. me outlet 2 of the slag quench vessel l is connected by any suitable connecting line 3 to a lockhopper 4 located below the said slag quench vessel. In the line 3 one or more valves 3a are provided.
In the lockhopper 4 a pprm~npnt gas bubble or gascap 5 is maintained, at a pressure lower than the pressure in the slag quench vessel l. The gas bubble may for example consist of an inert gas such as nitrogen.
The lockhopper 4 is provided with an outlet 7 at its bottom and one or mnre valves 7a for discharging the solidified slag from the gasification system during a sluicing cycle. m e slag can be discharged to any means suitable for the purpose (not shown for reasons of clarity). The gas bubble 5 in the lockhopper may be maintained by supplying inert gas (such as nitrogen) to the lockho~per 4 by means of a conduit or pipe 6 penetrating into the upper interior space of the lockhopper, as shown in fig. l, or advantageously by means of a pipe 6a in fluid communication with the vertically disposed conduit between the slag quench vessel l and the lockhopper 4, as shown in fig. 2, and wherein said vertical conduit penetrates into the interior of said lockh~ppPr a distance sufficient to maintain the gas bubble in the ll~pprmnst part of the lockhopper.
m e operation of the system of the invention is as follows:
the liquid slag which is formed in the gasification system during the partial combustion process falls into the water bath or slag quench vessel l where it soli~ifies.
From the slag quench vessel l it falls by gravity into the lockhopper 4 from which the solidified slag is batchwise sluiced out of the gasification system. It will be clear to those skilled in the art that at ~Lu~Liate times the valves 3a and 7a should be opened and closed respectively.
~uring the sluicing cycle the lockhopper 4 is isolated from -the g~ific~tion system since the valves 3a between the slag quench vessel and the lockhopper are closed, whereas the valves 7a at the outlet 7 of the lockhopper 4 are opened. m us, slag which is produced in the meantime, will collect in the slag quench vessel 1 above the valves 3a and has a tendency for bridging at the narrow space just abcve these valves ( schematically represented by the bridging region A).
According to the invention, after reconnecting the lockhopper 4 to the gasification system by closing the valves 7a and opening the valves 3a the gas bubble in the lockhopper having a lower pressure than the pressure in the slag quench vessel creates an initial downwards flow of water and slag thus resulting in a debridging action in the region A.
It will be appreciated that the gas bubble also allows a quick performance test of the valves. If the volume of the gas bubble changes with time this is an indication of valve leakages.
It will further be appreciated that the pressure of the gas bubble in the lockhopper can be higher than the pressure of the discharge means outside the lockhopper. In this manner unloading of the lockhopper is facilitated and possible bridging at the outlet 7 of the lockhopper is reduced.
Various mn~if;c~tions of the present invention will hec~mP
apparent to those skilled in the art from the foregoing description and accompanying drawing. Such modifications are intended to fall within the scope of the ~pe~d claims.
Claims (6)
1. A process for the preparation of synthesis gas by partial combustion of finely divided solid carbon-containing fuel with an oxygen-containing gas in a reactor, wherein liquid slag formed during the partial combustion process falls into a water bath or slag quench vessel where it solidifies and from there falls by gravity into a lockhopper from which the solidified slag is batchwise sluiced out of the gasification system, said lock-hopper and slag quench vessel being connected through one or more valves, comprising the steps of creating and maintaining a gas bubble or gascap in the lockhopper, the pressure of the gas bubble being lower than the pressure in the slag quench vessel when the said one or more valves between the lockhopper and the slag quench vessel are closed, thus creating an initial downwards flow of water and slag during opening of the valves between the lockhopper and the slag quench vessel.
2. The process as claimed in claim 1 wherein the gas bubble is maintained by supplying gas to the lockhopper by means of a conduit or pipe extending into the upper interior space within the lockhopper.
3. The process as claimed in claim 1 or 2 wherein the gas bubble consists of an inert gas.
4. The process as claimed in claim 3 wherein the said inert gas is nitrogen.
5. An apparatus for carrying out the process as claimed in claim 1 comprising a slag quench vessel, connected through one or more valves to a lockhopper provided at its bottom with an outlet, comprising one or more valves, and means for creating and maintaining a gas bubble in the lockhopper.
6. The apparatus as claimed in claim 5 wherein said means for creating a gas bubble comprises a conduit or pipe extending into the upper interior space within the lockhopper.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DEP3714915.4 | 1987-05-05 | ||
| DE19873714915 DE3714915A1 (en) | 1987-05-05 | 1987-05-05 | METHOD AND DEVICE FOR THE PRODUCTION OF SYNTHESIS GAS |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1336645C true CA1336645C (en) | 1995-08-15 |
Family
ID=6326856
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA000564586A Expired - Lifetime CA1336645C (en) | 1987-05-05 | 1988-04-20 | Process and apparatus for the preparation of synthesis gas |
Country Status (7)
| Country | Link |
|---|---|
| EP (1) | EP0290087B1 (en) |
| JP (1) | JP2609533B2 (en) |
| CN (1) | CN1018187B (en) |
| AU (1) | AU599786B2 (en) |
| CA (1) | CA1336645C (en) |
| DE (2) | DE3714915A1 (en) |
| ZA (1) | ZA883134B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20100288711A1 (en) * | 2008-01-24 | 2010-11-18 | Uhde Gmhh | Method and system for removing slag, particularly slag that occurs during synthesis gas extraction, from a slag bath container |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AU764501B2 (en) * | 1999-09-21 | 2003-08-21 | Air Products And Chemicals, Inc. | Process to remove solid slag particles from a mixture of solid slag particles and water |
| US6755980B1 (en) | 2000-09-20 | 2004-06-29 | Shell Oil Company | Process to remove solid slag particles from a mixture of solid slag particles and water |
| CN101061204B (en) | 2004-11-22 | 2011-01-12 | 国际壳牌研究有限公司 | Apparatus for gasifying fuel |
| CN101003358B (en) | 2006-12-12 | 2011-05-18 | 华东理工大学 | Multi nozzle gasification furnace feeding in hydrocarbon-including plasma or powder state |
| CN1994865B (en) | 2006-12-12 | 2011-05-18 | 华东理工大学 | Gasification device for two-stage gasification coupled with heat recovery and washing and its uses |
| US8349170B2 (en) * | 2008-05-14 | 2013-01-08 | Exxonmobil Research And Engineering Company | FCC reactor and riser design for short contact-time catalytic cracking of hydrocarbons |
| DE102008033095A1 (en) | 2008-07-15 | 2010-01-28 | Uhde Gmbh | Apparatus for slag removal from a coal gasification reactor |
| DE102008033094A1 (en) | 2008-07-15 | 2010-01-28 | Uhde Gmbh | Gasification device with continuous solids discharge |
| DE102008035386A1 (en) | 2008-07-29 | 2010-02-11 | Uhde Gmbh | Slag discharge from reactor for syngas recovery |
| CN118667586A (en) * | 2024-08-21 | 2024-09-20 | 国家电投集团山西电力有限公司 | Auxiliary component of biomass gasification furnace |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3235313A (en) * | 1964-05-18 | 1966-02-15 | Koppers Co Inc | Sluicing solid materials from spaces under superatmospheric pressure |
| DE2455127C2 (en) * | 1974-11-21 | 1986-02-27 | Shell Internationale Research Maatschappij B.V., Den Haag | Process for discharging residues from a gasification chamber under increased pressure |
| BR8105270A (en) * | 1980-11-12 | 1982-08-31 | Texaco Development Corp | PROCESS FOR THE PRODUCTION OF SYNTHESIS GAS SUBSTANTIALLY FREE OF PARTICLES |
| US4533363A (en) * | 1984-01-20 | 1985-08-06 | Texaco Development Corporation | Production of synthesis gas |
| DE3507628A1 (en) * | 1985-03-05 | 1986-09-18 | Veba Oel Entwicklungs-Gesellschaft mbH, 4650 Gelsenkirchen | METHOD AND DEVICE FOR EJECTING ASHES OR ALSO SLAG PARTIES FROM A PRESSURE GASIFICATION REACTOR |
| JPS61243896A (en) * | 1985-04-23 | 1986-10-30 | Mitsubishi Heavy Ind Ltd | Method of discharging slag in gasifying oven |
| CA1320642C (en) * | 1986-08-06 | 1993-07-27 | M. Dale Mayes | Slag removal system for a solid fuels gasification reactor |
-
1987
- 1987-05-05 DE DE19873714915 patent/DE3714915A1/en not_active Withdrawn
-
1988
- 1988-04-20 CA CA000564586A patent/CA1336645C/en not_active Expired - Lifetime
- 1988-04-27 DE DE8888200829T patent/DE3860637D1/en not_active Expired - Fee Related
- 1988-04-27 EP EP88200829A patent/EP0290087B1/en not_active Expired - Lifetime
- 1988-05-02 JP JP63107781A patent/JP2609533B2/en not_active Expired - Lifetime
- 1988-05-03 AU AU15525/88A patent/AU599786B2/en not_active Expired
- 1988-05-03 ZA ZA883134A patent/ZA883134B/en unknown
- 1988-05-03 CN CN88102581A patent/CN1018187B/en not_active Expired
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20100288711A1 (en) * | 2008-01-24 | 2010-11-18 | Uhde Gmhh | Method and system for removing slag, particularly slag that occurs during synthesis gas extraction, from a slag bath container |
| US8414780B2 (en) * | 2008-01-24 | 2013-04-09 | Thyssenkrupp Uhde Gmbh | Method and system for removing slag, particularly slag that occurs during synthesis gas extraction, from a slag bath container |
Also Published As
| Publication number | Publication date |
|---|---|
| EP0290087A3 (en) | 1989-02-08 |
| EP0290087B1 (en) | 1990-09-19 |
| JP2609533B2 (en) | 1997-05-14 |
| ZA883134B (en) | 1988-11-08 |
| DE3860637D1 (en) | 1990-10-25 |
| CN88102581A (en) | 1988-11-16 |
| DE3714915A1 (en) | 1988-11-24 |
| AU1552588A (en) | 1988-11-10 |
| JPS63286493A (en) | 1988-11-24 |
| CN1018187B (en) | 1992-09-09 |
| AU599786B2 (en) | 1990-07-26 |
| EP0290087A2 (en) | 1988-11-09 |
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